CN109096113B - Method for aromatizing synthetic oak moss - Google Patents

Method for aromatizing synthetic oak moss Download PDF

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CN109096113B
CN109096113B CN201811067935.6A CN201811067935A CN109096113B CN 109096113 B CN109096113 B CN 109096113B CN 201811067935 A CN201811067935 A CN 201811067935A CN 109096113 B CN109096113 B CN 109096113B
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dimethyl
dioxo
oak moss
aromatizing
reaction
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CN109096113A (en
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李军
高志国
魏小纪
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Lanzhou Fuersheng Technology Development Co ltd
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Tianjin Ankaite Technology Development Co ltd
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    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C67/00Preparation of carboxylic acid esters
    • C07C67/30Preparation of carboxylic acid esters by modifying the acid moiety of the ester, such modification not being an introduction of an ester group
    • C07C67/333Preparation of carboxylic acid esters by modifying the acid moiety of the ester, such modification not being an introduction of an ester group by isomerisation; by change of size of the carbon skeleton
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C67/00Preparation of carboxylic acid esters
    • C07C67/30Preparation of carboxylic acid esters by modifying the acid moiety of the ester, such modification not being an introduction of an ester group
    • C07C67/307Preparation of carboxylic acid esters by modifying the acid moiety of the ester, such modification not being an introduction of an ester group by introduction of halogen; by substitution of halogen atoms by other halogen atoms
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2601/00Systems containing only non-condensed rings
    • C07C2601/12Systems containing only non-condensed rings with a six-membered ring
    • C07C2601/14The ring being saturated

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  • Organic Chemistry (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

The invention provides a method for aromatizing synthetic oak moss, which comprises the steps of adding chlorinated 3, 6-dimethyl-2, 4-dioxo-methyl cyclohexanecarboxylate into acetonitrile serving as a solvent for aromatization reaction, and then cooling and crystallizing to obtain a synthetic oak moss crude product. Compared with the prior art, the method for aromatizing the synthetic oak moss has the following advantages: 1. the by-product sodium chloride generated by the reaction can be directly filtered out; 2. the water of reaction can be recycled; 3. during aromatization reaction, the reaction is not violent because the aromatization reaction is carried out in acetonitrile solvent, and the generated hydrogen chloride is easy to recover; 4. the post-treatment process is simple, and the purity of the produced crude product is up to more than 98%. Therefore, the method provides an improved process method for synthesizing the oak moss, which is environment-friendly, energy-saving and capable of realizing industrial production.

Description

Method for aromatizing synthetic oak moss
Technical Field
The invention belongs to the field of fine chemical engineering, and relates to an improved method for aromatizing synthetic spice, in particular to a method for aromatizing synthetic oak moss.
Background
The oak moss has unique oak moss-like fragrance and good fragrance-fixing agent, and is widely applied to perfumed soaps, detergents, high-grade perfumes and tobaccos. In the past, natural oak moss extract is used, and the oak moss extract is discolored by alkali and is difficult to prepare soap essence. The synthetic oak moss has no such disadvantages.
The present synthesis method of oak moss is reported in West German patent publication 2, 359, 233(1974) that dimethyl malonate is used as raw material, and condensed in methanol solution of sodium methoxide to obtain dihydro oak moss intermediate, which is then aromatized by using reagents such as N-bromocaprolactone amine, etc. and its reaction time is long and cost is high. West German patent publication 2,653,177 (1978) aromatizes waste acid with inexpensive reagents such as acetic anhydride, concentrated sulfuric acid, etc.
International flavor and essence company patent CN106631794A A preparation method of oak moss crystal flavor adopts one-pot synthesis method to synthesize oak moss crystal, the method uses methanol as solvent and water, the produced salt water has bad color, and methanol is used for aromatization to produce methyl chloride, because the boiling point of methyl chloride is only-22 deg.C, it is not suitable for recovery.
Disclosure of Invention
In view of the above, the present invention aims to provide a new method for improving the aromatization of synthetic oak moss to solve the problems in the prior art.
In order to achieve the purpose, the technical scheme of the invention is realized as follows:
the method comprises the steps of adding chlorinated 3, 6-dimethyl-2, 4-dioxo-methyl cyclohexanecarboxylate into acetonitrile serving as a solvent for aromatization reaction, and then cooling and crystallizing to obtain a crude product of the synthesized oak moss.
Further, the aromatization reaction is carried out under the condition of 60-90 ℃ for 4-20 hours, wherein the weight ratio of the 3, 6-dimethyl-2, 4-dioxo-cyclohexane methyl chloride to the acetonitrile is 1 (1-5).
Further, the preparation method of the chlorinated 3, 6-dimethyl-2, 4-dioxo-cyclohexanecarboxylic acid methyl ester comprises the following steps: (1) 4-hexene-3-ketone and dimethyl malonate are subjected to Michael addition reaction and intramolecular claisen condensation reaction under the condition of sodium methoxide, and then acid acidification and suction filtration are carried out to obtain 3, 6-dimethyl-2, 4-dioxo-methyl cyclohexanecarboxylate;
(2) adding 3, 6-dimethyl-2, 4-dioxo-cyclohexane methyl formate into water and chloralkane, and introducing chlorine gas to carry out chlorination reaction.
Further, in the step (2), the weight ratio of the 3, 6-dimethyl-2, 4-dioxo-cyclohexanecarboxylic acid methyl ester to the water is 1: (1-5).
Further, in the step (2), the weight ratio of the 3, 6-dimethyl-2, 4-dioxo-cyclohexane methyl formate to the chloralkane is 1: (1-5), wherein the chloroalkane is dichloromethane, chloroform or carbon tetrachloride.
Further, the acidification process in the step (1) is to adopt hydrochloric acid with the mass fraction of 30%, and the saturated saline solution obtained after acidification is filtered and recycled.
Further, hydrogen chloride generated in the aromatization process is absorbed by water and then is used in an acidification process in the preparation method of the 3, 6-dimethyl-2, 4-dioxo-methyl cyclohexanecarboxylate.
Further, hydrogen chloride generated in the aromatization process is absorbed by three stages of water, wherein one stage is saturated absorption and is used for an acidification procedure in the preparation method of the 3, 6-dimethyl-2, 4-dioxo-methyl cyclohexanecarboxylate.
Compared with the prior art, the method for aromatizing the synthetic oak moss has the following advantages:
1. the by-product sodium chloride generated by the reaction can be directly filtered out; 2. the water of reaction can be recycled; 3. during aromatization reaction, the reaction is not violent because the aromatization reaction is carried out in acetonitrile solvent, and the generated hydrogen chloride is easy to recover; 4. the post-treatment process is simple, and the purity of the produced crude product is up to more than 98%. Therefore, the method provides an improved process method for synthesizing the oak moss, which is environment-friendly, energy-saving and capable of realizing industrial production.
Detailed Description
Unless defined otherwise, technical terms used in the following examples have the same meanings as commonly understood by one of ordinary skill in the art to which the present invention belongs. The test reagents used in the following examples, unless otherwise specified, are all conventional biochemical reagents; the experimental methods are conventional methods unless otherwise specified.
The technical scheme of the invention is that 2, 5-dimethyl-dihydro-beta-methyl-fulminate is separated in water and chloralkane, chlorine is introduced for chlorination reaction, reaction liquid is separated after the chlorination reaction is finished, saturated saline water is filtered for recycling, and filtered sodium chloride is sold as a byproduct. After the reaction liquid is recovered by the solvent, acetonitrile is added as the solvent, aromatization reaction is carried out at the temperature of 55-90 ℃, and the generated hydrogen chloride is absorbed and then acidified for recycling. After the reaction is finished, the crude oak moss product with the content of more than 98 percent is obtained by suction filtration, and the acetonitrile is recycled.
Wherein, the raw material 3, 6-dimethyl-2, 4-dioxo-cyclohexane methyl formate is solid obtained by carrying out Michael addition acidification on dimethyl malonate and 4-hexene-3-ketone. The specific chemical reaction formula is as follows:
Figure GDA0003007862540000041
the present invention will be described in detail with reference to examples.
Example 1
Putting 200g of 3, 6-dimethyl-2, 4-dioxo-cyclohexane methyl formate, 400g of water and 400g of dichloromethane into a 2000ml four-mouth bottle, introducing 800g of chlorine gas at 0-25 ℃, separating an organic phase, collecting the dichloromethane in the organic phase, adding 300g of acetonitrile, aging at 80 ℃ for 5 hours, recovering 200g of acetonitrile, cooling and suction-filtering to obtain a crude product of oak moss, drying a filter cake to obtain 113g of a product with the purity of 98.2% and the yield of 90.9%.
Example 2
200g of methyl 3, 6-dimethyl-2, 4-dioxo-cyclohexanecarboxylate (containing sodium chloride neutralized by Michael addition reaction), 400g of dichloromethane and water separated in example 1 were put into a 2000ml four-necked flask, 800g of chlorine gas was introduced at 0 to 25 ℃, then the organic phase was separated, dichloromethane in the organic phase was collected, 600g of acetonitrile was added, reaction was carried out at 85 ℃ for 10 hours, 450g of acetonitrile was recovered, crude synthetic oak moss was obtained by cooling and suction filtration, and the crude synthetic oak moss was dried to obtain 112.5g of a product with a purity of 98.1% and a yield of 90.5%.
Example 3
200g of methyl 3, 6-dimethyl-2, 4-dioxo-cyclohexanecarboxylate (containing sodium chloride neutralized by Michael addition reaction), 600g of dichloromethane and water separated in example 2 are added into a 2000ml four-necked flask, 800g of chlorine gas is introduced at 0-25 ℃, then an organic phase is separated, sodium chloride is filtered from an aqueous phase to completely recover dichloromethane in the organic phase, 900g of acetonitrile is added for reacting for 18 hours at 86 ℃, 790g of acetonitrile is recovered, the temperature is reduced to 10 ℃, then crude oak moss is obtained by suction filtration, and 110g of a product with the purity of 98.6 percent and the yield of 88.5 percent is obtained after drying.
The above description is only for the purpose of illustrating the preferred embodiments of the present invention and is not to be construed as limiting the invention, and any modifications, equivalents, improvements and the like that fall within the spirit and principle of the present invention are intended to be included therein.

Claims (8)

1. A method for aromatizing synthetic oak moss is characterized by comprising the following steps: adding chlorinated 3, 6-dimethyl-2, 4-dioxo-methyl cyclohexanecarboxylate into acetonitrile serving as a solvent for aromatization reaction, and then cooling and crystallizing to obtain a synthesized oak moss crude product;
the chlorinated 3, 6-dimethyl-2, 4-dioxo-cyclohexanecarboxylic acid methyl ester has the formula:
Figure FDA0003010326030000011
2. a process for the aromatization of synthetic oak moss according to claim 1 wherein: the aromatization reaction is carried out under the condition of 60-90 ℃ for 4-20 hours, wherein the weight ratio of the 3, 6-dimethyl-2, 4-dioxo-cyclohexane methyl chloride to the acetonitrile is 1 (1-5).
3. A process for aromatizing synthetic oak moss according to claim 1 or 2 wherein: the preparation method of the chlorinated 3, 6-dimethyl-2, 4-dioxo-methyl cyclohexanecarboxylate comprises the following steps: (1) 4-hexene-3-ketone and dimethyl malonate are subjected to Michael addition reaction and intramolecular claisen condensation reaction under the condition of sodium methoxide, and then acid acidification and suction filtration are carried out to obtain 3, 6-dimethyl-2, 4-dioxo-methyl cyclohexanecarboxylate;
(2) adding 3, 6-dimethyl-2, 4-dioxo-cyclohexane methyl formate into water and chloralkane, and introducing chlorine gas to carry out chlorination reaction.
4. A process of aromatizing synthetic oak moss according to claim 3 wherein: in the step (2), the weight ratio of the 3, 6-dimethyl-2, 4-dioxo-cyclohexanecarboxylic acid methyl ester to the water is 1: (1-5).
5. A process for aromatizing synthetic oak moss according to claim 3 wherein: in the step (2), the weight ratio of the 3, 6-dimethyl-2, 4-dioxo-cyclohexane methyl formate to the chloralkane is 1: (1-5), wherein the chloroalkane is dichloromethane, chloroform or carbon tetrachloride.
6. A process of aromatizing synthetic oak moss according to claim 3 wherein: the acidification process in the step (1) is to adopt hydrochloric acid with the mass fraction of 30%, and the saturated salt water obtained after acidification is recycled after filtration.
7. A process of aromatizing synthetic oak moss according to claim 3 wherein: the hydrogen chloride generated in the aromatization process is absorbed by water and then is used in the acidification procedure of the preparation method of the 3, 6-dimethyl-2, 4-dioxo-methyl cyclohexanecarboxylate.
8. A process for aromatizing synthetic oak moss according to claim 7 wherein: the hydrogen chloride generated in the aromatization process is absorbed by three stages of water, wherein the first stage is saturated absorption and is used for the acidification procedure in the preparation method of the 3, 6-dimethyl-2, 4-dioxo-methyl cyclohexanecarboxylate.
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Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3634491A (en) * 1968-08-30 1972-01-11 Int Flavors & Fragrances Inc Process for the preparation of 3 5-dialkyl resorcylic acids and esters
US3884843A (en) * 1974-01-31 1975-05-20 Fritzsche Dodge & Olcott Inc Alkyl monomethyl-ringsubstituted-diacetoxy-benzoate perfume compositions
CN86100869A (en) * 1986-01-10 1987-07-22 中国科学院上海有机化学研究所 The chemosynthesis of the main essence of oak moss
CN102351706A (en) * 2011-08-04 2012-02-15 江苏中烟工业有限责任公司 Method for synthesizing ethyldivaricatinate and application of ethyldivaricatinate
CN106631794A (en) * 2016-09-28 2017-05-10 国际香料和香精公司 Process for preparing perfume 2,5-dimethylmethyl resorcylate

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3634491A (en) * 1968-08-30 1972-01-11 Int Flavors & Fragrances Inc Process for the preparation of 3 5-dialkyl resorcylic acids and esters
US3884843A (en) * 1974-01-31 1975-05-20 Fritzsche Dodge & Olcott Inc Alkyl monomethyl-ringsubstituted-diacetoxy-benzoate perfume compositions
CN86100869A (en) * 1986-01-10 1987-07-22 中国科学院上海有机化学研究所 The chemosynthesis of the main essence of oak moss
CN102351706A (en) * 2011-08-04 2012-02-15 江苏中烟工业有限责任公司 Method for synthesizing ethyldivaricatinate and application of ethyldivaricatinate
CN106631794A (en) * 2016-09-28 2017-05-10 国际香料和香精公司 Process for preparing perfume 2,5-dimethylmethyl resorcylate

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